EP0317739B1 - Use of amine compounds for preparing low density silicone foam - Google Patents

Use of amine compounds for preparing low density silicone foam Download PDF

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Publication number
EP0317739B1
EP0317739B1 EP88116251A EP88116251A EP0317739B1 EP 0317739 B1 EP0317739 B1 EP 0317739B1 EP 88116251 A EP88116251 A EP 88116251A EP 88116251 A EP88116251 A EP 88116251A EP 0317739 B1 EP0317739 B1 EP 0317739B1
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use according
carbon atoms
radicals
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substituted
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EP0317739A3 (en
EP0317739A2 (en
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Frank Joseph Modic
Richard Ambert Striker
Wayne Lee Delker
Richard Karl Sammel
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General Electric Co
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General Electric Co
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0014Use of organic additives
    • C08J9/0042Use of organic additives containing silicon
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0014Use of organic additives
    • C08J9/0028Use of organic additives containing nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/02Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by the reacting monomers or modifying agents during the preparation or modification of macromolecules
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2383/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen, or carbon only; Derivatives of such polymers
    • C08J2383/04Polysiloxanes

Definitions

  • the present invention relates to low density silicone foam. More particularly, the present invention relates to low density silicone foam which is produced by simultaneous vinyl addition and hydride/hydroxy reactions in the presence of certain amine compounds.
  • Elastomeric silicone foams are well known and have a variety of uses, including thermal insulation, electrical insulation, flame barrier, cushioning applications, etc. Elastomeric silicone foams have excellent physical properties and in addition to the above uses are suitable and desirable for use in many additional applications. However, there is a problem with elastomeric silicone foam that it is expensive and at 240-400 kg/m 3 (15-25 lb/ft 3 ), the ability to reduce price is limited by the basic costs of silicone material.
  • U.S. Pat. No. 3,923,705 discloses that elastomeric silicone foams may be produced with a single reaction that both cross-links to cure the composition as well as produces hydrogen gas to blow the foam. This reaction takes place between a silanol and silicon hydride.
  • a vinyl containing silicone that will simultaneously cross-link through addition with a silicon hydride without gas generation. Obviously, this is a convenient method to produce silicone foam. It is also true, however, that gas generation must be proportional to cross-linking or cure rate and therefore density is difficult to control.
  • Modic produces silicone foam compositions by adding water.
  • water could be added to a composition of a vinyl containing siloxane, a hydride containing siloxane and platinum to generate gas at a rate only indirectly related to cross-linking rate.
  • the water reacts with hydride containing siloxane to produce hydrogen gas and silanol.
  • Silanol reacts with hydride containing siloxane to cross-link and produce a second molecule of hydrogen gas.
  • a vinyl addition reaction with silicone hydride will cross-link the composition simultaneously.
  • a major advantage of Modic is that gas is produced without the addition of silanol and with only small amounts of water.
  • U.S. Pat. No. 4,418,157 Modic, reduces density and strengthens silicone foam by adding a resinous copolymer.
  • U.S. Pat. No. 4,599,367, Baumann, et al. reduces density by using a combination of silanol and water, or a monohydroxyl alcohol.
  • US-A-4584361 discloses that a specified group of monoalkylamines and alkylenediamines, wherein the alkyl or alkylene group contains from two to four carbon atoms, imparts long term storage stability at temperatures of up to 40°C to one part polyorganosiloxane compositions curable by a platinum catalyzed hydrosilation reaction.
  • the inhibitors do not interfere with the ability of these compositions to cure rapidly at temperatures of 135°C to form gels that are useful encapsulating materials for delicate devices, including electronic circuits.
  • EP-A-0223409 discloses a method of producing elastomeric silicone foam comprising mixing a vinyl-containing polydiorganosiloxane (1), a hydroxylated polydiorganosiloxane (2), a platinum catalyst (3), an organohydrogensiloxane (4) and a profoamer (5), allowing a froth to form and curing at ambient temperature to an elastomeric silicone foam.
  • the profoamer is a resinous, benzene-soluble organosiloxane copolymer consisting of SiO 4/2 units, silicone-bonded hydroxyl groups, (CH 3 ) 3 SiO 1/2 units, and fluorine-containing units.
  • a liquified blowing agent may be used and the mixture stirred under superatmospheric pressure, forming a foam by releasing the mixture to atmospheric pressure.
  • elastomeric silicone foams in use so that the self-blowing characteristics can be retained yet controlled independently of cure. It is also desirable that appropriate cell size be maintained with increased gas generation and that foam strength and other physical properties are not more than proportionally effected at lower elastomeric silicone foam densities.
  • the present invention relates to the use in a foamable composition
  • a foamable composition comprising:
  • R and R 1 may be substituted or unsubstituted hydrocarbon radicals of from 1 to 20 carbon atoms with the proviso that there is controlled vinyl substitutiion and controlled viscosity.
  • the vinyl substitution should range from about 0.0002 to 3% by weight and preferably, from about 0.001 to about 1% by weight.
  • Viscosity should vary from about 100 to about 1,000,000 mPa s (centipoise) at 25°C and preferably, from about 2500 to 500,000 mPa.s (centipoise).
  • the more limited vinyl concentration given above will allow for a reaction that proceeds at an appropriate rate, that is not too slow and allows for proper cross-linking in the polymer to produce cured elastomeric silicone foam.
  • the viscosity it is preferred that the viscosity not be too high, otherwise the composition is difficult to handle and will not foam well.
  • the vinyl-containing polymer will form the major part of the foamable composition and thus the viscosity will be important to the viscosity of the final composition.
  • Substituted or unsubstituted hydrocarbon radicals of R and R 1 may be selected from alkyl radicals, methyl, ethyl, propyl, etc.; cycloalkyl radicals such as cyclohexyl, cycloheptyl, etc; mononuclear aryl radicals such as phenyl, methyl phenyl and ethylphenyl; alkenyl radicals such as vinyl, allyl, etc. and more preferably vinyl and other well known substituent groups for diorganopolysiloxane polymers.
  • R and R 1 radicals are selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, aryl radicals such as phenyl; vinyl radicals and halogenated hydrocarbon radicals such as fluoroalkyl radicals of 3 to 8 carbon atoms, such-as, for instance 3,3,3-trifluoropropyl.
  • R 1 radicals are selected from methyl radicals, phenyl radicals, vinyl radicals and 3,3,3-trifluoropropyl radicals where the polymer has the foregoing vinyl substitution and R is vinyl.
  • vinyl-containing polysiloxane where the vinyl units appear only on the siloxane chain can be used to produce silicone foam, the physical properties are not as good as where there is terminal vinyl substitution.
  • a particularly preferred polymer has only terminal vinyl substitution, i.e. where R is vinyl and R 1 is methyl, phenyl, and/or 3,3,3-trifluoropropyl.
  • Vinyl-containing polysiloxanes are well known in the art and may be produced by a variety of methods, for instance, by equilibrating cyclic polysiloxanes with or without vinyl substitution in the presence of appropriate amounts of vinyl substituted chainstopper. Further details for production of vinyl-substituted polysiloxanes may be found in U.S. Pat. No. 3,425,967 to Modic. Further suitable vinyl-containing polysiloxanes may be found in U.S. Pat. No. 4,599,367; 4,418,157 and 3,923,705.
  • component (a) For each 100 parts by weight of vinyl-containing polysiloxane, component (a), there should be present in the foamable composition from about 1 to 50 parts by weight of hydride polysiloxane, component (b), and preferably, from about 5 to 30 parts by weight.
  • R 2 may be independently hydrogen, an alkyl radical of from 1 to 8 carbon atoms, an aryl radical from 1 to 8 carbon atoms or a haloalkyl radical of 3 to 8 carbon atoms or simultaneously a single -0- to form a cyclic polymer and R 3 may be selected from the same radicals as R 2 absent hydrogen and oxygen.
  • the hydride polysiloxane have a hydrogen content ranging from about 0.3 to about 1.6% by weight and as shown in formula (2), z and y vary to provide a viscosity ranging from 1 to 500 centipoise at 25°C.
  • the hydride content is not critical but such a content substantially less than about 0.3% by weight of the hydride polysiloxane may not provide sufficient hydrogen in the foamable composition to react with the hydroxy source and liberate hydrogen gas as well as react and cross-link with vinyl molecules of the vinyl-containing polysiloxane. The result will of course be a poorly blown and undercured foam.
  • viscosity of the hydride polysiloxane is not critical, but higher viscosity materials may be difficult to obtain and utilize.
  • viscosity ranges from about 5 to about 250 centipoise at 25°C and most preferably from about 5 to 100 centipoise.
  • the hydride polysiloxane contain hydrogen on the siloxane chain. It is optional that hydrogen atoms are a substituent on terminal siloxy atoms. If there are no hydrogen atoms in the polymer chain of the hydride polysiloxanes, then a proper silicone foam is not obtained. Accordingly, a hydride polymer with only hydrogen radicals on terminal siloxy atoms will not work to form a silicone foam in the composition of the instant case.
  • a hydroxyl source is necessary to properly blow the foamable composition.
  • the source of hydroxyl may be selected from any of water, organic alcohol or silanol or mixtures thereof.
  • Suitable silanols include any hydroxylated organosiloxane or hydroxylated organosiloxane mixture having an average of 1 to 2.5 silicon-bonded hydroxyl radicals per molecule.
  • the organo radicals can be any radical described above for R and R 1 .
  • the silanols may be homopolymers, copolymers or mixtures thereof. It is preferred that the silanol contain at least one organic radical in a molecule per silicon atom.
  • silanols examples include hydroxyl end-blocked polydimethylsiloxane, hydroxyl end-blocked polydiorganosiloxane having siloxane units of dimethylsiloxane and phenylmethylsiloxane, hydroxyl end-blocked polymethyl-3,3,3-trifluoropropylsiloxane and hydroxyl end-blocked polyorganosiloane having siloxane units of monomethylsiloxane, dimethylsiloxane, with the monomethylsiloxane units supplying "on-chain" hydroxyl groups.
  • the silanol also includes mixtures of hydroxylated organosiloxane polymers and hydroxylated organosilanes, such as mixture of hydroxyl end-blocked polydimethylsiloxane and diphenylmethylsilanol.
  • Organic alcohols suitable for use herein may be substituted or unsubstituted, mono or polyols, preferably having from about 1 to 12 carbon atoms. Substituent groups may serve to increase the solubility of the alcohol or to improve the dispersability of an insoluble species.
  • Preferred organic alcohols include ethanol, propanol, butanol, lauryl alcohol, octyl alcohol and ethylene glycol.
  • Each of the above enumerated hydroxyl sources may react with hydrogen of the hydride polysiloxane to produce hydrogen gas.
  • this reaction is common and required of any hydroxyl source utilized, the by-product of the reaction may differ and produce other benefits or require attention as known to the art.
  • Water will react with the hydride function to produce a hydroxyl function which can further react with a second hydride to produce additional gas and a cross-link site.
  • additional gas will be generated as a benefit, but gassing after cure may occur.
  • Silanol due to good solubility in the composition characteristically produces gas immediately but may lead to problems of premature gelation.
  • Organic alcohol does not as easily react with the hydride function and thus is generally used in silanol or water combinations.
  • this ratio is broadly stated, particularly at the upper boundary in view of the fact that hydride functions must be available to react with vinyl functions for cross-linking and should not be consumed by hydroxy functions.
  • the hydroxyl function to hydride function ratio may also be high.
  • the ratio of hydroxyl radicals to hydride radicals should vary between about 0.02/1 to 10/1 and more preferably between about 0.5/1 to about 7/1.
  • Suitable platinum compound for use as the catalyst herein are well known.
  • the preferred platinum catalysts are soluble in the present reaction mixture.
  • the platinum compound can be selected from those having the formula (PtCl 2 .Olefin) 2 and H(PtCl 3 .Olefin) as described in U.S. Pat. No. 3,159,601, Ashby.
  • the olefin shown in the previous two formulas can be almost any type of olefin but is preferably an alkenylene having from 2 to 8 carbon atoms, a cycloalkenylene having from 5 to 7 carbon atoms or styrene.
  • Specific olefins utilizable in the above formulas are ethylene, propylene, the various isomers of butylene, octylene, cyclopentane, cyclohexene and cycloheptene.
  • a further platinum containing material usable in the composition of the present invention is the platinum chloride cyclopropane complex (PtCl 2 C 3 H 6 ) 2 described in U.S. Pat. No. 3,159,662, Ashby. Still further, the patent containing material can be a complex formed from chloroplatinic acid with up to 2 moles per gram of platinum of a member selected from the class consisting of alcohols, ethers, aldehydes and mixtures of the above as described in U.S. Pat. No. 3,220,972, Lamoreaux.
  • the preferred platinum compound to be used not only as a platinum catalyst, but also as a flame retardant additive is that disclosed in U.S. Pat. No. 3,775,452, Karstedt.
  • this type of platinum complex is formed by reacting chloroplatinic acid containing 4 moles of water of hydration with tetramethyltetravinylcyclosiloxane in the presence of sodium bicarbonate in an ethanol solution.
  • the compounds suitable and effective to lower foam density have the general formula: NR 4 3 where R 4 is selected from the group consisting of hydrogen, hydroxyl, substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 16 carbon atoms, or a substituted or unsubstituted silyl.
  • R 4 is selected from the group consisting of hydrogen, hydroxyl, substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 16 carbon atoms, or a substituted or unsubstituted silyl.
  • R 4 is selected from the group consisting of hydrogen, hydroxyl, substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 16 carbon atoms, or a substituted or unsubstituted silyl.
  • up to one R 4 may be hydroxy and up to two R 4 may be hydrogen or at least one R 4 must be selected from substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 18 carbon atoms, and substituted or unsubstituted silyl.
  • Suitable compounds characterized by R 4 being silyl include compounds where R 4 is a substituted or unsubstituted silyl hydrocarbon or monovalent silicone polymer.
  • R 4 is a substituted or unsubstituted silyl hydrocarbon or monovalent silicone polymer.
  • Preferred such compounds are the silyl hydrocarbon type including hexamethyldisilazane, (CH 3 ) 3 SiNHCH 3 , (CH 3 ) 3 SiNHC 2 H 5 , ((CH 3 ) 3 Si) 2 NCH 3 , ((C 2 H 5 ) 3 Si) 2 NH, ((CH 3 ) 2 SiNH) 3 .
  • R 4 may join to form cyclic structures.
  • the amine (e) be soluble in foamable composition.
  • a soluble amine compound will be more easily dispersed and, of course, if totally soluble have no discrete micelles to hinder contact with the composition. It is preferred that the amine have a solubility in components (a) and (b) ranging from about 0.1 millimole/liter to infinitely soluble.
  • a large amount of compound (e) in the foamable composition is neither necessary nor desirable. Therefore, there should be added from 0.007 to 1 parts by weight compound (e) based on 100 parts by weight components (a), (b) and (c). Preferably there are added from 0.007 to 0.1 parts compound (e) as above.
  • the foamable composition herein may contain from 0 to 200 parts by weight by a filler, which may be either an extending or reinforcing filler.
  • a filler which may be either an extending or reinforcing filler.
  • extending fillers are preferred since reinforcing filler such as fumed silica and precipitated silica when incorporated into the composition in any concentration unduly increase the viscosity of the composition, thus making it difficult to handle and to pour.
  • fumed silica and precipitated silica have the advantages of increasing the physical properties, that is, the tensile strength as well as the tear of the silicone elastomeric foam that is formed from the composition.
  • filler based on 100 parts of the vinyl-containing base polymer.
  • the filler may be selected from the class consisting of reinforcing fillers and extending fillers, and more preferably just extending fillers.
  • a preferred extending filler that may be utilized in the instant composition which does not unduly increase the viscosity of the uncured composition is ground quartz. Ground quartz has the additional advantage that to some extent it increases the burn resistance properties of the cured silicone foam that is produced from the composition.
  • extending fillers that may be utilized in the instant compositions are, for instance, titanium dioxide, lithopone, zinc oxide, zirconium silicate, silica aerogel, iron oxide, diatomaceous earth, calcium carbonate, glass fibers, magnesium oxide, chromic oxide, zirconium oxide, aluminum oxide, alpha quartz, calcined clay, carbon and, graphite.
  • reinforcing fillers such as fumed silica and precipitated silica, that in order to keep the viscosity increase in the composition as low as possible such filler, even the extending fillers, may be treated, for instance, with cyclicpolysiloxanes or silazanes.
  • silica fillers may be treated, for instance, with cyclicpolysiloxanes is set forth in U.S.-A-2,938,009.
  • Another method of treating reinforcing fillers is, for instance, to be found in Brown, U.S. Pat. No. 3,024,126, U.S.-A-3,635,743 and, U.S.-A-3,837,878.
  • Such ingredients such as cyclicpolysiloxanes may also be utilized to treat extending fillers such as, ground quartz, with some advantage since such treatment does also alleviate the viscosity increase caused by extending fillers.
  • the most preferred filler for utilization to produce silicone foam of the instant case is ground quartz. Quartz enhances the burn resistant properties of the composition as well as imparting some enhanced physical properties to the final cured silicone foam.
  • the foamable composition is generally used and stored as a two-part composition.
  • the platinum catalyst is incorporated, preferably, in the vinyl-containing polysiloxane.
  • the hydroxyl source may be added to the vinyl-containing polysiloxane and incorporated in the hydride polysiloxane. Again, preferably, the hydroxyl source is incorporated into the vinyl-containing polysiloxane to prevent a chance of premature reaction, and since there is more vinyl-containing material, the incorporation is easier. It should also be appreciated that the hydroxyl source could constitute a third component.
  • the amine compound like the platinum catalyst, should be incorporated into the vinyl-containing polysiloxane.
  • the amine compound may be dispersed on the surface of a filler and so added to the appropriate part of the composition.
  • the amine compound is dispersed on a filler by simply dipping or spraying the filler with imine compound or solution and subsequently drying with gentle heat or vacuum.
  • the hydride polysiloxane is rapidly mixed with the vinyl-containing polysiloxane containing the hydroxyl source, platinum, and amine compound, and the composition is poured into the desired cavity and allowed to stand.
  • the composition will begin to crosslink and generate gas simultaneously to blow and cure to an elastomeric silicone foam having a density of less than 224 kg/m 3 (14 lb./ft. 3 ).
  • an inhibitor it is desirably used at least 200 parts per million based on the total composition of an inhibitor including a vinyl-containing cyclictetrasiloxane such as tetra methyl tetra-vinylcyclopolysiloxane, malleates or vinyl acetylene compounds.
  • a vinyl-containing cyclictetrasiloxane such as tetra methyl tetra-vinylcyclopolysiloxane, malleates or vinyl acetylene compounds.
  • inhibitors are added to the composition at a concentration of anywhere from 100 parts per million to 10,000 parts per million based on the total composition so as to give to the composition work life varying anywhere from 5 to 20 minutes at room temperature. Smaller amounts of inhibitor does not give an appreciable increase of work life at room temperature of the composition and larger amounts of the inhibitor may be used than 10,000 parts per million, per weight of the composition. However such has not been found to be necessary.
  • additives for foam are well known. Carbon black, pigment, glass fibers, etc. may be added according to the skill of the art. Particularly preferred additives are MQ or MDQ resins with vinyl functions to lower density and increase strength. The addition of these resins is described in U.S. Pat. No. 4,418,157.
  • a two part foamable composition was mixed as follows. Gel time is the time required for the foam to begin to become elastomeric in character.
  • Part A Polymer/Filler Parts by Weight Vinyl terminated polydimethylsiloxane mixture with MD vinyl Q resin, total viscosity 30,000 cps at 25°C, 0.5% vinyl 73 Ground quartz 25 Calcium Carbonate 2 Karstedt platinum catalyst 40 ppm Pt H 2 O 1.5
  • Part B Polymer Parts by Weight Poly-dimethyl-methylhydrogen siloxane, 1.5% by weight hydrogen 66 Vinyl terminated polydimethylsiloxane 85,000 cps @ 25°C 34
  • Part A is blended with (CH 3 CH 2 ) 2 NOH, diethylhydroxyl amine, to form a foamable composition in the amounts shown in Table 1 and poured into a mold at room temperature.
  • the diethylhydroxyl amine, DEHA is blended with Part A.

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Description

  • The present invention relates to low density silicone foam. More particularly, the present invention relates to low density silicone foam which is produced by simultaneous vinyl addition and hydride/hydroxy reactions in the presence of certain amine compounds.
  • Background of the Invention
  • Elastomeric silicone foams are well known and have a variety of uses, including thermal insulation, electrical insulation, flame barrier, cushioning applications, etc. Elastomeric silicone foams have excellent physical properties and in addition to the above uses are suitable and desirable for use in many additional applications. However, there is a problem with elastomeric silicone foam that it is expensive and at 240-400 kg/m3 (15-25 lb/ft3), the ability to reduce price is limited by the basic costs of silicone material.
  • The technical advances necessary to significantly reduce the basic cost of silicone material are not on the horizon, thus it is clear that to immediately reduce the cost of elastomeric silicone foam it is necessary to reduce the density of the foam. Although this may seem to be a simple matter of adding additional blowing agent, etc., it is an aspect of elastomeric silicone foam as presently used that density is not easily lowered. The reasons for this are apparent with a review of silicone foam technology.
  • U.S. Pat. No. 3,923,705, Smith, discloses that elastomeric silicone foams may be produced with a single reaction that both cross-links to cure the composition as well as produces hydrogen gas to blow the foam. This reaction takes place between a silanol and silicon hydride. Optionally, there can be added a vinyl containing silicone that will simultaneously cross-link through addition with a silicon hydride without gas generation. Obviously, this is a convenient method to produce silicone foam. It is also true, however, that gas generation must be proportional to cross-linking or cure rate and therefore density is difficult to control.
  • U.S. Pat. No. 4,189,545, Modic, produces silicone foam compositions by adding water. For example, water could be added to a composition of a vinyl containing siloxane, a hydride containing siloxane and platinum to generate gas at a rate only indirectly related to cross-linking rate. The water reacts with hydride containing siloxane to produce hydrogen gas and silanol. Silanol reacts with hydride containing siloxane to cross-link and produce a second molecule of hydrogen gas. A vinyl addition reaction with silicone hydride will cross-link the composition simultaneously. Thus, a major advantage of Modic is that gas is produced without the addition of silanol and with only small amounts of water.
  • U.S. Pat. No. 4,418,157, Modic, reduces density and strengthens silicone foam by adding a resinous copolymer. U.S. Pat. No. 4,599,367, Baumann, et al., reduces density by using a combination of silanol and water, or a monohydroxyl alcohol.
  • US-A-4584361 discloses that a specified group of monoalkylamines and alkylenediamines, wherein the alkyl or alkylene group contains from two to four carbon atoms, imparts long term storage stability at temperatures of up to 40°C to one part polyorganosiloxane compositions curable by a platinum catalyzed hydrosilation reaction. The inhibitors do not interfere with the ability of these compositions to cure rapidly at temperatures of 135°C to form gels that are useful encapsulating materials for delicate devices, including electronic circuits.
  • EP-A-0223409 discloses a method of producing elastomeric silicone foam comprising mixing a vinyl-containing polydiorganosiloxane (1), a hydroxylated polydiorganosiloxane (2), a platinum catalyst (3), an organohydrogensiloxane (4) and a profoamer (5), allowing a froth to form and curing at ambient temperature to an elastomeric silicone foam. The profoamer is a resinous, benzene-soluble organosiloxane copolymer consisting of SiO4/2 units, silicone-bonded hydroxyl groups, (CH3)3SiO1/2 units, and fluorine-containing units. A liquified blowing agent may be used and the mixture stirred under superatmospheric pressure, forming a foam by releasing the mixture to atmospheric pressure.
  • Accordingly, it is desirable to modify the elastomeric silicone foams in use so that the self-blowing characteristics can be retained yet controlled independently of cure. It is also desirable that appropriate cell size be maintained with increased gas generation and that foam strength and other physical properties are not more than proportionally effected at lower elastomeric silicone foam densities.
  • Therefore, it is an object of the present invention to produce an elastomeric silicone foam having a reduced density.
  • It is another object of the present invention to produce such a foam with uniform cells and comparatively good strength and elongation.
  • It is yet another object of the present invention to produce a method to reduce the density of elastomeric silicone foam.
  • These and other objects of the present invention are accomplished by means of the disclosure set forth hereinbelow.
  • Summary of the Invention
  • Briefly, the present invention relates to the use in a foamable composition comprising:
    • (a) 100 parts by weight of a vinyl-containing polysiloxane of the formula:
      Figure imgb0001
      where R and R1 are selected from substituted or unsubstituted hydrocarbon radicals of from 1 to 20 carbon atoms, such that the polymer contains from 0.0002 to 3% by weight vinyl and x varies such that the viscosity of the polymer varies from 100 to 1,000,000 mPa·s (centipoise) at 25°C;
    • (b) from 1 to 50 parts by weight of a hydride polysiloxane of the formula:
      Figure imgb0002
      where R2 is selected from the group consisting of, independently, hydrogen, alkyl radicals of from 1 to 8 carbon atoms, aryl radicals of from 1 to 8 carbon atoms, haloalkyl radicals of 3 to 8 carbon atoms and simultaneously a single -0- to form a cyclic polymer, and R3 is selected from the group consisting of alkyl radicals of from 1 to 8 carbon atoms, aryl radicals of from 1 to 8 carbon atoms, and fluoroalkyl radicals of 3 to 8 carbon atoms, where the hydride polysiloxane has a hydrogen content varying from 0.3 to 1.6% by weight and z and y vary such that the polymer has a viscosity varying from 1 to 500 centipoise at 25°C;
    • (c) a hydroxyl source selected from the group consisting of water, organic alcohol, hydroxylated siloxane, and combinations thereof, excluding compounds according to (e), in an amount to provide a molar ratio of from 0.02/1 to 15/1 of hydroxyl radicals to silicon-bonded hydrogen atoms of component (b) ; and
    • (d) from about 1 to about 250 parts per million of platinum catalyst; of a foam density reducing component
    • (e) from 0.007 to 1 part by weight per 100 parts by weight of (a), (b) and (c) of a compound of the formula : NR 4 3
      Figure imgb0003
      wherein R4 is selected from the group consisting of hydrogen, hydroxy, substituted or unsubstituted alkyl of 1 to 18 carbon atoms, substituted or unsubstituted aryl of 1 to 18 carbon atoms and a substituted or unsubstituted silyl hydrocarbon or monovalent silicone polymer, wherein ammonia is excluded.
    Detailed Description of the Invention
  • In the vinyl-containing polysiloxane, component (a) as shown in formula (1) R and R1 may be substituted or unsubstituted hydrocarbon radicals of from 1 to 20 carbon atoms with the proviso that there is controlled vinyl substitutiion and controlled viscosity. The vinyl substitution should range from about 0.0002 to 3% by weight and preferably, from about 0.001 to about 1% by weight. Viscosity should vary from about 100 to about 1,000,000 mPa s (centipoise) at 25°C and preferably, from about 2500 to 500,000 mPa.s (centipoise). Although a polymer having a broader range of vinyl content will operate in the present invention, the more limited vinyl concentration given above will allow for a reaction that proceeds at an appropriate rate, that is not too slow and allows for proper cross-linking in the polymer to produce cured elastomeric silicone foam. With respect to the preferred range of viscosity, as can be appreciated, it is preferred that the viscosity not be too high, otherwise the composition is difficult to handle and will not foam well. The vinyl-containing polymer will form the major part of the foamable composition and thus the viscosity will be important to the viscosity of the final composition.
  • Substituted or unsubstituted hydrocarbon radicals of R and R1 may be selected from alkyl radicals, methyl, ethyl, propyl, etc.; cycloalkyl radicals such as cyclohexyl, cycloheptyl, etc; mononuclear aryl radicals such as phenyl, methyl phenyl and ethylphenyl; alkenyl radicals such as vinyl, allyl, etc. and more preferably vinyl and other well known substituent groups for diorganopolysiloxane polymers. Preferably the R and R1 radicals are selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, aryl radicals such as phenyl; vinyl radicals and halogenated hydrocarbon radicals such as fluoroalkyl radicals of 3 to 8 carbon atoms, such-as, for instance 3,3,3-trifluoropropyl. Most preferably R1 radicals are selected from methyl radicals, phenyl radicals, vinyl radicals and 3,3,3-trifluoropropyl radicals where the polymer has the foregoing vinyl substitution and R is vinyl. Although vinyl-containing polysiloxane where the vinyl units appear only on the siloxane chain can be used to produce silicone foam, the physical properties are not as good as where there is terminal vinyl substitution. A particularly preferred polymer has only terminal vinyl substitution, i.e. where R is vinyl and R1 is methyl, phenyl, and/or 3,3,3-trifluoropropyl.
  • Vinyl-containing polysiloxanes are well known in the art and may be produced by a variety of methods, for instance, by equilibrating cyclic polysiloxanes with or without vinyl substitution in the presence of appropriate amounts of vinyl substituted chainstopper. Further details for production of vinyl-substituted polysiloxanes may be found in U.S. Pat. No. 3,425,967 to Modic. Further suitable vinyl-containing polysiloxanes may be found in U.S. Pat. No. 4,599,367; 4,418,157 and 3,923,705.
  • For each 100 parts by weight of vinyl-containing polysiloxane, component (a), there should be present in the foamable composition from about 1 to 50 parts by weight of hydride polysiloxane, component (b), and preferably, from about 5 to 30 parts by weight. As shown above in formula (2), R2 may be independently hydrogen, an alkyl radical of from 1 to 8 carbon atoms, an aryl radical from 1 to 8 carbon atoms or a haloalkyl radical of 3 to 8 carbon atoms or simultaneously a single -0- to form a cyclic polymer and R3 may be selected from the same radicals as R2 absent hydrogen and oxygen. It is preferred that the hydride polysiloxane have a hydrogen content ranging from about 0.3 to about 1.6% by weight and as shown in formula (2), z and y vary to provide a viscosity ranging from 1 to 500 centipoise at 25°C. The hydride content is not critical but such a content substantially less than about 0.3% by weight of the hydride polysiloxane may not provide sufficient hydrogen in the foamable composition to react with the hydroxy source and liberate hydrogen gas as well as react and cross-link with vinyl molecules of the vinyl-containing polysiloxane. The result will of course be a poorly blown and undercured foam. Likewise, viscosity of the hydride polysiloxane is not critical, but higher viscosity materials may be difficult to obtain and utilize. Preferably, viscosity ranges from about 5 to about 250 centipoise at 25°C and most preferably from about 5 to 100 centipoise.
  • As seen in formula (2) above, it is critical that the hydride polysiloxane contain hydrogen on the siloxane chain. It is optional that hydrogen atoms are a substituent on terminal siloxy atoms. If there are no hydrogen atoms in the polymer chain of the hydride polysiloxanes, then a proper silicone foam is not obtained. Accordingly, a hydride polymer with only hydrogen radicals on terminal siloxy atoms will not work to form a silicone foam in the composition of the instant case.
  • A hydroxyl source is necessary to properly blow the foamable composition. The source of hydroxyl may be selected from any of water, organic alcohol or silanol or mixtures thereof.
  • Suitable silanols include any hydroxylated organosiloxane or hydroxylated organosiloxane mixture having an average of 1 to 2.5 silicon-bonded hydroxyl radicals per molecule. The organo radicals can be any radical described above for R and R1. The silanols may be homopolymers, copolymers or mixtures thereof. It is preferred that the silanol contain at least one organic radical in a molecule per silicon atom. Examples of suitable silanols include hydroxyl end-blocked polydimethylsiloxane, hydroxyl end-blocked polydiorganosiloxane having siloxane units of dimethylsiloxane and phenylmethylsiloxane, hydroxyl end-blocked polymethyl-3,3,3-trifluoropropylsiloxane and hydroxyl end-blocked polyorganosiloane having siloxane units of monomethylsiloxane, dimethylsiloxane, with the monomethylsiloxane units supplying "on-chain" hydroxyl groups. The silanol also includes mixtures of hydroxylated organosiloxane polymers and hydroxylated organosilanes, such as mixture of hydroxyl end-blocked polydimethylsiloxane and diphenylmethylsilanol.
  • Organic alcohols suitable for use herein may be substituted or unsubstituted, mono or polyols, preferably having from about 1 to 12 carbon atoms. Substituent groups may serve to increase the solubility of the alcohol or to improve the dispersability of an insoluble species. Preferred organic alcohols include ethanol, propanol, butanol, lauryl alcohol, octyl alcohol and ethylene glycol.
  • Each of the above enumerated hydroxyl sources may react with hydrogen of the hydride polysiloxane to produce hydrogen gas. Although this reaction is common and required of any hydroxyl source utilized, the by-product of the reaction may differ and produce other benefits or require attention as known to the art. Water will react with the hydride function to produce a hydroxyl function which can further react with a second hydride to produce additional gas and a cross-link site. Thus, where water is employed, additional gas will be generated as a benefit, but gassing after cure may occur. Silanol, due to good solubility in the composition characteristically produces gas immediately but may lead to problems of premature gelation. Organic alcohol does not as easily react with the hydride function and thus is generally used in silanol or water combinations. Silanol and water combinations have also been found particularly beneficial. Persons skilled in the art are familiar with each of the above. For further teaching there are U.S. Pat. Nos. 4,189,545; 4,418,157; 4,599,367; and 3,923,705.
  • Depending on the hydroxyl source used there should be from about 0.02/1 to about 15/1 moles hydroxyl radicals employed from the hydroxyl source for each silicon-bonded hydrogen atom in the hydride polysiloxane of component (b). Of course, this ratio is broadly stated, particularly at the upper boundary in view of the fact that hydride functions must be available to react with vinyl functions for cross-linking and should not be consumed by hydroxy functions. However, where water or difunctional hydroxyl compounds are used and much cross-linking takes place through hydroxy/hydride reactions or where vinyl concentration is very high, then the hydroxyl function to hydride function ratio may also be high. Preferably however, the ratio of hydroxyl radicals to hydride radicals should vary between about 0.02/1 to 10/1 and more preferably between about 0.5/1 to about 7/1.
  • Suitable platinum compound for use as the catalyst herein are well known. The preferred platinum catalysts are soluble in the present reaction mixture. The platinum compound can be selected from those having the formula (PtCl2.Olefin)2 and H(PtCl3.Olefin) as described in U.S. Pat. No. 3,159,601, Ashby. The olefin shown in the previous two formulas can be almost any type of olefin but is preferably an alkenylene having from 2 to 8 carbon atoms, a cycloalkenylene having from 5 to 7 carbon atoms or styrene. Specific olefins utilizable in the above formulas are ethylene, propylene, the various isomers of butylene, octylene, cyclopentane, cyclohexene and cycloheptene.
  • A further platinum containing material usable in the composition of the present invention is the platinum chloride cyclopropane complex (PtCl2C3H6)2 described in U.S. Pat. No. 3,159,662, Ashby. Still further, the patent containing material can be a complex formed from chloroplatinic acid with up to 2 moles per gram of platinum of a member selected from the class consisting of alcohols, ethers, aldehydes and mixtures of the above as described in U.S. Pat. No. 3,220,972, Lamoreaux.
  • The preferred platinum compound to be used not only as a platinum catalyst, but also as a flame retardant additive is that disclosed in U.S. Pat. No. 3,775,452, Karstedt. Generally speaking, this type of platinum complex is formed by reacting chloroplatinic acid containing 4 moles of water of hydration with tetramethyltetravinylcyclosiloxane in the presence of sodium bicarbonate in an ethanol solution.
  • Finally, in the process of the instant case there is utilized generally from 1 to 250 parts per million of a platinum catalyst and more preferably 1 to 200 parts per million of a platinum catalyst. It is more preferred to utilize a stabilized platinum complex in the process of the instant case since it disperses in the ingredients much more easily and as such results in faster reaction time.
  • The compounds suitable and effective to lower foam density have the general formula: NR 4 3
    Figure imgb0004
    where R4 is selected from the group consisting of hydrogen, hydroxyl, substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 16 carbon atoms, or a substituted or unsubstituted silyl. As is well known in the art, amine compounds where more than one group is hydroxy are unstable and difficult to manufacture. Further, ammonia is not generally known as an amine. Thus, up to one R4 may be hydroxy and up to two R4 may be hydrogen or at least one R4 must be selected from substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 18 carbon atoms, and substituted or unsubstituted silyl.
  • Suitable amine compounds characterized by R4 being hydroxyl, substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, or substituted or unsubstituted aryl of from 1 to 18 carbon atoms include hydroxy amines, for example, diethyl hydroxyl amine and primary secondary and tertiary amines, for example, H2NC3H6Si (OEt)3, H2NC3H6NHC3H6Si(OCH3)3, (Me2N)2-C=NC3H6Si(OCH3)3, (Me2N)2-C=NC4H9, tetramethylpiperidine, piperidine, N-Methylmorpholine, N,N-dimethylethylenediamine, N-Methylipiperidine, N-hexylamine, tributylamine, dibutylamine, cyclohexylamine, Di-n-hexylamine, triethylamine, benzylamine, dipropylamine, N-ethylphenylamine, dimethyl soya amines, tetramethyl guanidine, and N-methylmorpholine.
  • Suitable compounds characterized by R4 being silyl include compounds where R4 is a substituted or unsubstituted silyl hydrocarbon or monovalent silicone polymer. Preferred such compounds are the silyl hydrocarbon type including hexamethyldisilazane, (CH3)3SiNHCH3, (CH3)3SiNHC2H5, ((CH3)3Si)2NCH3, ((C2H5)3Si)2NH, ((CH3)2SiNH)3. As seen, R4 may join to form cyclic structures.
  • It is preferred that the amine (e) be soluble in foamable composition. A soluble amine compound will be more easily dispersed and, of course, if totally soluble have no discrete micelles to hinder contact with the composition. It is preferred that the amine have a solubility in components (a) and (b) ranging from about 0.1 millimole/liter to infinitely soluble.
  • A large amount of compound (e) in the foamable composition is neither necessary nor desirable. Therefore, there should be added from 0.007 to 1 parts by weight compound (e) based on 100 parts by weight components (a), (b) and (c). Preferably there are added from 0.007 to 0.1 parts compound (e) as above.
  • Optionally the foamable composition herein may contain from 0 to 200 parts by weight by a filler, which may be either an extending or reinforcing filler. It should be noted that extending fillers are preferred since reinforcing filler such as fumed silica and precipitated silica when incorporated into the composition in any concentration unduly increase the viscosity of the composition, thus making it difficult to handle and to pour. However, fumed silica and precipitated silica have the advantages of increasing the physical properties, that is, the tensile strength as well as the tear of the silicone elastomeric foam that is formed from the composition.
  • Accordingly in the more referred embodiment of the instant case there is utilized from 10 to 100 parts of filler based on 100 parts of the vinyl-containing base polymer. The filler may be selected from the class consisting of reinforcing fillers and extending fillers, and more preferably just extending fillers. A preferred extending filler that may be utilized in the instant composition which does not unduly increase the viscosity of the uncured composition is ground quartz. Ground quartz has the additional advantage that to some extent it increases the burn resistance properties of the cured silicone foam that is produced from the composition. Other extending fillers that may be utilized in the instant compositions are, for instance, titanium dioxide, lithopone, zinc oxide, zirconium silicate, silica aerogel, iron oxide, diatomaceous earth, calcium carbonate, glass fibers, magnesium oxide, chromic oxide, zirconium oxide, aluminum oxide, alpha quartz, calcined clay, carbon and, graphite.
  • It should be noted if reinforcing fillers are used such as fumed silica and precipitated silica, that in order to keep the viscosity increase in the composition as low as possible such filler, even the extending fillers, may be treated, for instance, with cyclicpolysiloxanes or silazanes. The disclosure in which silica fillers may be treated, for instance, with cyclicpolysiloxanes is set forth in U.S.-A-2,938,009. However, such is only one method of treating reinforcing fillers and other methods with other agents are also available in the art.
  • Another method of treating reinforcing fillers is, for instance, to be found in Brown, U.S. Pat. No. 3,024,126, U.S.-A-3,635,743 and, U.S.-A-3,837,878. Such ingredients such as cyclicpolysiloxanes may also be utilized to treat extending fillers such as, ground quartz, with some advantage since such treatment does also alleviate the viscosity increase caused by extending fillers. However, as stated previously, the most preferred filler for utilization to produce silicone foam of the instant case, is ground quartz. Quartz enhances the burn resistant properties of the composition as well as imparting some enhanced physical properties to the final cured silicone foam.
  • The foamable composition is generally used and stored as a two-part composition. The platinum catalyst is incorporated, preferably, in the vinyl-containing polysiloxane. The hydroxyl source may be added to the vinyl-containing polysiloxane and incorporated in the hydride polysiloxane. Again, preferably, the hydroxyl source is incorporated into the vinyl-containing polysiloxane to prevent a chance of premature reaction, and since there is more vinyl-containing material, the incorporation is easier. It should also be appreciated that the hydroxyl source could constitute a third component. The amine compound, like the platinum catalyst, should be incorporated into the vinyl-containing polysiloxane. The amine compound may be dispersed on the surface of a filler and so added to the appropriate part of the composition. The amine compound is dispersed on a filler by simply dipping or spraying the filler with imine compound or solution and subsequently drying with gentle heat or vacuum.
  • When it is desired to form the silicone foam, the hydride polysiloxane is rapidly mixed with the vinyl-containing polysiloxane containing the hydroxyl source, platinum, and amine compound, and the composition is poured into the desired cavity and allowed to stand. The composition will begin to crosslink and generate gas simultaneously to blow and cure to an elastomeric silicone foam having a density of less than 224 kg/m3 (14 lb./ft.3).
  • It is sometimes desired to have a certain amount of work life or pot life in the mixed composition prior to its cure. Accordingly, for such purposes, it is normal to use an inhibitor. It has been found that to the compositions of the instant case there is desirably used at least 200 parts per million based on the total composition of an inhibitor including a vinyl-containing cyclictetrasiloxane such as tetra methyl tetra-vinylcyclopolysiloxane, malleates or vinyl acetylene compounds. When added to the composition inhibitors give the composition some work life or pot life. Preferably inhibitors are added to the composition at a concentration of anywhere from 100 parts per million to 10,000 parts per million based on the total composition so as to give to the composition work life varying anywhere from 5 to 20 minutes at room temperature. Smaller amounts of inhibitor does not give an appreciable increase of work life at room temperature of the composition and larger amounts of the inhibitor may be used than 10,000 parts per million, per weight of the composition. However such has not been found to be necessary.
  • Of course additional additives for foam are well known. Carbon black, pigment, glass fibers, etc. may be added according to the skill of the art. Particularly preferred additives are MQ or MDQ resins with vinyl functions to lower density and increase strength. The addition of these resins is described in U.S. Pat. No. 4,418,157.
  • Examples
  • The examples below are given for the purpose of illustrating the practice of the above invention. All parts are by weight.
  • Examples 1-7
  • A two part foamable composition was mixed as follows. Gel time is the time required for the foam to begin to become elastomeric in character.
    Part A
    Polymer/Filler Parts by Weight
    Vinyl terminated polydimethylsiloxane mixture with MDvinyl Q resin, total viscosity 30,000 cps at 25°C, 0.5% vinyl 73
    Ground quartz 25
    Calcium Carbonate 2
    Karstedt platinum catalyst 40 ppm Pt
    H2O 1.5
    Part B
    Polymer Parts by Weight
    Poly-dimethyl-methylhydrogen siloxane, 1.5% by weight hydrogen 66
    Vinyl terminated polydimethylsiloxane 85,000 cps @ 25°C 34
  • A 10:1 ratio of Part A: Part B is blended with (CH3CH2)2NOH, diethylhydroxyl amine, to form a foamable composition in the amounts shown in Table 1 and poured into a mold at room temperature. In blending the foamable composition, the diethylhydroxyl amine, DEHA, is blended with Part A. Table 1
    Example ppm DEHA Gel time (sec.) Rise time (min.) Density (lbs/ft3) Kg/M3
    1* 0 165 10 15.2 243.5
    2* 30 300 10 14.3 229.1
    3 70 360 9 11.5 184.2
    4 140 360 9 11.1 177.8
    5 260 375 10 10.4 166.6
    6 400 375 11 10.5 168.2
    7 750 415 11 13.7 219.5
    * Comparative
  • Examples 8-12
  • The procedure and ingredients of Examples 1-7 were repeated except DEHA was replaced with the compounds and amounts shown in Table 2. Table 2
    Example Additive ppm of Additive Gel time, sec. Rise time, min. Density (lbs/ft3) Kg/m3
    8+ - - 165 10 15.3 245.1
    9 DEHA 100 360 9 11.0 176.2
    10 *IPA 100 300 11 12.8 205.0
    11 **HMDZ 100 225 9 13.6 217.9
    12 ***TEA 100 225 9 14.0 224.3
    * Isopropylamine
    ** Hexamethyldisilazane
    *** Triethanolamine
    + comparative

Claims (20)

  1. The use in a foamable composition comprising :
    (a) 100 parts by weight of a vinyl-containing polysiloxane of the formula :
    Figure imgb0005
    where R and R1 are selected from substituted or unsubstituted hydrocarbon radicals of from 1 to 20 carbon atoms, such that the polymer contains from 0.0002 to 3% by weight vinyl and x varies such that the viscosity of the polymer varies from 100 to 1,000,000 mPa.S (centipoise) at 25°C;
    (b) from 1 to 50 parts by weight of a hydride polysiloxane of the formula :
    Figure imgb0006
    where R2 is selected from the group consisting of independently, hydrogen, alkyl radicals of from 1 to 8 carbon atoms, aryl radicals of from 1 to 8 carbon atoms, haloalkyl radicals of 3 to 8 carbon atoms and simultaneously, a single -O-to form a cyclic polymer and R3 is selected from the group consisting of alkyl radicals of from 1 to 8 carbon atoms, aryl radicals of from 1 to 8 carbon atoms, and fluoroalkyl radicals of 3 to 8 carbon atoms, where the hydride polysiloxane has a hydrogen content varying from 0.3 to 1.6% by weight and z and y vary such that the polymer has a viscosity varying from 1 to 500 mPa.s (centipoise) at 25°C;
    (c) a hydroxyl source selected from the group consisting of water, organic alcohol , hydroxylated siloxane, and combinations thereof, excluding compounds according to (e), in an amount to provide a molar ratio of from about 0.02/1 to about 15/1 of hydroxyl radicals to silicon-bonded hydrogen atoms of component (b); and
    (d) from 1 to 250 parts per million of platinum catalyst; of a foam density reducing component
    (e) from 0.007 to 1 part by weight per 100 parts by weight of components (a), (b) and (c) of a compound of the formula : NR 4 3
    Figure imgb0007
    wherein R4 is selected from the group consisting of hydrogen, hydroxy, substituted or unsubstituted alkyl of 1 to 18 carbon atoms substituted or unsubstituted aryl of 6 to 18 carbon atoms, and a substituted or unsubstituted silyl hydrocarbon or monovalent silicone polymer, wherein ammonia is excluded.
  2. The use according to Claim 1 wherein said vinyl-containing polysiloxane contains from 0.001 to 1% by weight vinyl.
  3. The use according to Claim 1 wherein said x varies such that the viscosity of the polymer varies from 2500 to 500,000 mPa.s (centipoise) at 25°C.
  4. The use according to Claim 1 wherein R and R1 are selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, aryl radicals, vinyl radicals and halogenated hydrocarbon radicals of 3 to 8 carbon atoms.
  5. The use according to Claim 1 wherein R is vinyl and R1 is selected from the group consisting of methyl, phenyl and 3,3,3-trifluoropropyl.
  6. The use according to Claim 1 wherein the composition contains from 5 to 30 parts by weight component (b).
  7. The use according to Claim 1 wherein said hydride polysiloxane has a viscosity between 5 and 100 mPa.s (centipoise) at 25°C.
  8. The use according to Claim 1 wherein said hydroxyl source is selected from the group consisting of water and combinations of water with organic alcohol or hydroxylated siloxane.
  9. The use according to Claim 1 wherein said hydroxyl source is selected from the group consisting of hydroxylated siloxane and combinations of hydroxylated siloxane with water or organic alcohol.
  10. The use according to Claim 1 wherein said hydroxylated siloxane has an average of from greater than 1 to 2.5 silicon-bonded hydroxyl radicals per molecule.
  11. The use according to Claim 1 wherein said organic alcohol is a substituted or unsubstituted alcohol having from 1 to 12 carbon atoms.
  12. The use according to Claim 11 wherein organic alcohol is selected from the group consisting of ethanol, propanol, butanol, lauryl alcohol, octyl alcohol and ethylene glycol.
  13. The use according to Claim 1 wherein the ratio of hydroxyl radicals to hydride radicals varies between 0.02/1 and 10/1.
  14. The use according to Claim 1 wherein at most one R4 is hydroxy and at least one R4 is selected from the group consisting of substituted or unsubstituted alkyl of from 1 to 18 carbon atoms, substituted or unsubstituted aryl of from 1 to 18 carbon atoms and substituted or unsubstituted silyl.
  15. The use according to Claim 1 wherein component (e) has a solubility in components (a) and (b) ranging upward from 0.1 millimole/liter.
  16. The use according to Claim 1 wherein component (e) is present in an amount of 0.007 to 0.1 parts by weight.
  17. The use according to Claim 1 wherein said substituted or unsubstituted silyl is a substituted or unsubstituted silyl hydrocarbon.
  18. The use according to Claim 10 wherein component (e) is selected from the group consisting of diethylhydroxylamine, isopropylamine, hexamethyldisilazane and triethanolamine.
  19. The use according to Claim 1 wherein the composition consists essentially of components (a) to (e) as claimed in Claim 1 and (f) from 0 to 200 parts by weight of filler.
  20. The use according to Claim 19 wherein the composition contains from 10 to 100 parts by weight of filler.
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DE3855767D1 (en) 1997-03-06
KR970006759B1 (en) 1997-04-30
KR890006756A (en) 1989-06-15
BR8805504A (en) 1989-07-04
ES2097735T3 (en) 1997-04-16
DE3855767T2 (en) 1997-07-24
EP0317739A2 (en) 1989-05-31

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